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WO2001085414A1 - Procede de delaminage - Google Patents

Procede de delaminage Download PDF

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Publication number
WO2001085414A1
WO2001085414A1 PCT/AU2001/000538 AU0100538W WO0185414A1 WO 2001085414 A1 WO2001085414 A1 WO 2001085414A1 AU 0100538 W AU0100538 W AU 0100538W WO 0185414 A1 WO0185414 A1 WO 0185414A1
Authority
WO
WIPO (PCT)
Prior art keywords
metal
polymeric substrate
process according
flakes
water
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/AU2001/000538
Other languages
English (en)
Inventor
John Sydney Hall
Michael Scott Mcrae-Williams
Kenneth Heater
Mark R. HODGE
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
METSS Corp
Original Assignee
METSS Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by METSS Corp filed Critical METSS Corp
Priority to EP20010929117 priority Critical patent/EP1341654B1/fr
Priority to AU5600001A priority patent/AU5600001A/xx
Priority to CA002406600A priority patent/CA2406600C/fr
Priority to DE2001621795 priority patent/DE60121795T2/de
Priority to AU2001256000A priority patent/AU2001256000B2/en
Priority to US10/275,679 priority patent/US6793709B2/en
Publication of WO2001085414A1 publication Critical patent/WO2001085414A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/04—Disintegrating plastics, e.g. by milling
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/02—Separating plastics from other materials
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
    • B29B2017/001—Pretreating the materials before recovery
    • B29B2017/0021—Dividing in large parts
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/02—Separating plastics from other materials
    • B29B2017/0213—Specific separating techniques
    • B29B2017/0217—Mechanical separating techniques; devices therefor
    • B29B2017/0224—Screens, sieves
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/02—Separating plastics from other materials
    • B29B2017/0213—Specific separating techniques
    • B29B2017/0286—Cleaning means used for separation
    • B29B2017/0289—Washing the materials in liquids
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/04—Disintegrating plastics, e.g. by milling
    • B29B2017/0424—Specific disintegrating techniques; devices therefor
    • B29B2017/0436—Immersion baths
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/04—Disintegrating plastics, e.g. by milling
    • B29B2017/0424—Specific disintegrating techniques; devices therefor
    • B29B2017/0484—Grinding tools, roller mills or disc mills
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2069/00—Use of PC, i.e. polycarbonates or derivatives thereof, as moulding material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2705/00—Use of metals, their alloys or their compounds, for preformed parts, e.g. for inserts
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2705/00—Use of metals, their alloys or their compounds, for preformed parts, e.g. for inserts
    • B29K2705/02—Aluminium
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2705/00—Use of metals, their alloys or their compounds, for preformed parts, e.g. for inserts
    • B29K2705/08—Transition metals
    • B29K2705/14—Noble metals, e.g. silver, gold or platinum
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29L—INDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
    • B29L2017/00—Carriers for sound or information
    • B29L2017/001—Carriers of records containing fine grooves or impressions, e.g. disc records for needle playback, cylinder records
    • B29L2017/003—Records or discs
    • B29L2017/005—CD''s, DVD''s
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00—Technologies for solid waste management
    • Y02W30/50—Reuse, recycling or recovery technologies
    • Y02W30/52—Mechanical processing of waste for the recovery of materials, e.g. crushing, shredding, separation or disassembly
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00—Technologies for solid waste management
    • Y02W30/50—Reuse, recycling or recovery technologies
    • Y02W30/62—Plastics recycling; Rubber recycling

Definitions

  • the present invention relates to a process for recycling electronic scrap material such as optical recording media, for instance CDs and DVDs.
  • electronic scrap material such as optical recording media, for instance CDs and DVDs.
  • the process involves delamination of electronic scrap material in order to recover the constituent components of it.
  • optical recording media such as CDs and DNDs has increased enormously in recent years with applications in the computer and audio/visual entertainment industries.
  • These media typically include a metal, such as aluminium and/or precious metals (typically gold or a mixture containing gold) provided on a polymeric substrate such as a polycarbonate.
  • a metal such as aluminium and/or precious metals (typically gold or a mixture containing gold)
  • the metal is provided on the polymeric substrate as a thin metallic film.
  • a protective layer is usually formed on the outer surfaces, and acrylates such as polymethyl (meth)acrylates are commonly used in this respect.
  • These optical recording media have a relatively short life of only a few years as they may become superseded or outdated. This leads to a considerable waste stream.
  • Recycling methods which ' rely on physical rather than chemical mechanisms have also been applied. For example, attempts have been made to remove a metallic layer from a polymeric substrate by slicing or shaving techniques. However, with such techniques the throughput can be relatively low and thus uneconomic where a large number of articles are to be recycled. Additionally, for security reasons, manufacturers sometimes choose to cut articles to be recycled (e.g. CDs andi DNDs) into pieces prior to transportation to a recycling facility. Techniques such as slicing and shaving cannot be applied practically to the articles in cut form.
  • the present invention seeks to provide a process for recycling an electronic scrap material which does not involve hazardous or potentially harmful chemicals and which is thus environmentally friendly, has high throughput and does not rely on the material to be recycled being in unitary form.
  • the method is easy to perform and economic in practice.
  • the polymer component it is desired to recover does not significantly degrade during the recycling process so that production of a high grade recycled product may be achieved.
  • the present invention provides a process for recycling an electronic scrap material comprising a metal provided on a polymeric substrate, which method comprises: milling flaked electronic scrap material with a bead impact material in the presence of water to produce flakes of cleaned polymeric substrate; adding water to the milled material and separating the flakes of cleaned polymeric substrate from metal-containing material; dewatering and drying the flakes of cleaned polymeric substrate; and treating the metal-containing material to recover the metal.
  • milling is used to denote any process by which attrition of the surface of the flakes of scrap material by contact with the bead impact material may be achieved. Such attrition removes of surface layer(s) of the scrap material and is a fundamental aspect of the present invention.
  • the terms milling and attrition may be used interchangeably in addition to their usual meanings in the particle science industry.
  • the scrap material to be milled is in flake form.
  • the scrap material for example a CD or DND
  • This may be achieved using a conventional shredding machine or granulator.
  • shredding/granulation cuts the material cleanly without any bending or distortion so that the resultant flakes are planar (assuming the original unitary material is planar). Bending or distortion of the scrap material during shredding/granulation can lead to metal smearing of the polymeric substrate material and/or may reduce the efficiency of the subsequent milling operation due to shielding effects.
  • the scrap material may be cut into flakes at the intended site of recycling or it may be supplied to the site in flake form.
  • the process of the invention may include as preliminary steps the transportation of electronic scrap material to a flaking station followed by cutting the material into flakes.
  • the flakes may then be transported to a recycling station where subsequent processing is carried out in accordance with the steps of the invention already described. If the scrap material is provided as is to the site where recycling is to take place, flake preparation will obviously be required prior to the subsequent processing. It is envisaged that in practice the scrap material would be supplied to a recycling facility in flake form. Depending on the flake size, further cutting ofthe flakes may be required prior to processing.
  • the flake size prior to milling is usually in the range 1 to 20mm, for example 1 to 15mm, preferably 4 to 8mm and more preferably 4 to 6mm.
  • the optimum flake size will depend upon such factors as the size of the bead impact material used in the milling step. If the flake size is too small, valuable polymeric material may be lost as fines in downstream process steps.
  • the flake size has implications with respect to the size of bead impact material used in the milling step. Thus, for relatively large flakes, milling may be optimised using a different size bead impact material when compared with the size of bead impact material most suitable for attrition of smaller flakes.
  • the flake size falls within a narrow distribution so that a correspondingly narrow distribution of size of bead impact material may be used in the milling step.
  • a correspondingly narrow distribution of size of bead impact material may be used in the milling step.
  • at least 50 wt%, for instance at least 75 wt% of flakes have a size of 4-8mm, and preferably 4-6mm. It will be appreciated however that a given batch of flakes to be treated may well have a broad distribution of flake size, and to optimise the milling step, bead impact material having a range of particle sizes may be used.
  • the flakes to be processed may include a distribution of flake size such that it will be most efficient to mill flakes above a predetermined size with a first size of diameter bead impact material and to mill flakes at or below the predetermined size with a second size diameter of bead impact material.
  • This embodiment ofthe present invention would thus comprise the following steps:
  • the predetermined size is typically about 3mm.
  • the first size of bead impact material is usually greater than lOOO ⁇ m and the second size of bead impact material is usually less than lOOO ⁇ m.
  • the first attrition or intensive shear stage generally leads to 80-90% removal of metal from the polymeric substrate.
  • the process may comprise: transporting a waste stream of electronic scrap material to a flaking station; dividing the material into flakes at the flaking station; and transporting the flakes to a milling station.
  • the milling step may be performed using a bead impact material having a particle size as low as 50 ⁇ m. If the flake, or a significant proportion ofthe flake (for instance in excess of 50 wt%), has a particle size of 20mm the particle size ofthe bead impact material may be as high as 3mm.
  • the function of the bead material is to remove by attrition the metal, and any additional layer(s) overlying the metal, and one skilled in the art would be able to select a suitable bead impact material size, or distribution thereof, based on this intended function and the following description of other relevant operational parameters.
  • the bead impact material any material serving the intended function of removing the metal, and any additional layer(s) overlying the metal, may be used.
  • the bead impact material should have a suitable surface hardness. Interactions between individual flakes may also contribute to the attrition process.
  • the bead impact material is in the form of particles having irregular surfaces. It is also preferred that the bead impact material has a roughened rather than smooth surface. As the milling step takes place in water, the material should also be suitably stable in water.
  • the process of the invention will also typically be carried out at elevated temperature and it follows from this that the bead impact material should also have the necessary integrity at the maximum temperature at which the process is performed.
  • bead impact material examples include plastics, silicon-containing materials, ceramics and metal powders.
  • examples include pumice, sand, powdered glass, diatomaceous earth and silicon carbide. Such materials are commercially available. It is also possible to make use of commercially available scouring agents, such as Ajax and Jif, which include abrasive particles in a carrier fluid/paste. It is preferred to use pumice having a particle size of about 300 ⁇ m or less or silica having a particle size of about 150 ⁇ m or less.
  • the use of metals as bead impact material can sometimes lead to discolouration of the polymeric substrate due to smearing.
  • Ceramic materials exhibit excellent abrasive properties although this should be counterbalanced with their tendency to be brittle.
  • the polymeric material itself possibly recycled from the process described herein, as the bead impact material.
  • the bead impact material may be recycled polycarbonate.
  • the density of the bead impact material is not too dissimilar (+50%) from that of the polymeric substrate it is desired to recover.
  • the effect of this is that there is enhanced mixing and dispersion of the bead impact material and the flake. If the density of the bead impact material and polymeric substrate is substantially different, partitioning the two may occur resulting in less effective attrition.
  • the size of the bead impact material and the flake may also be matched to enhance mixing and dispersion ofthe two.
  • the quantity of bead impact material may vary based on the amount of flake material present, and this will affect the rate of attrition. Thus, where the proportion of bead impact material is high relative to the amount of flake present, the rate of removal of metal, and any overlying layer(s), is correspondingly high. However, the rate of attrition should also be balanced with the rate of wear of the material and/or apparatus that will likely ensue.
  • the weight ratio of bead impact material to flake is 1:30, for example 1 :20. In practice the weight ratio chosen will be influenced by the desired process time which in turn may be influenced by things such as electricity costs. An important aspect ofthe invention is that the milling step takes place in the presence of water.
  • the water functions as a lubricant and heat transfer medium as well as aiding transport of the milled products.
  • the high intensity attrition due to the bead impact material leads to rapid distortion and heating ofthe flake at the interface between the various layers present, for example at the metal/polymeric substrate interface, leading to loss of adhesion and delamination. It can also be likened to the cutting of oxidised paint for surfaces with a car polish.
  • the weight ratio of water to flake is from 1:3 to 3:1 and, preferably, 1:1. If the proportion of water is much in excess of this, the process ofthe invention works less efficiently.
  • the process of the invention may be carried out under ambient conditions of temperature and pressure, although it will be appreciated that the milling step will itself cause a temperature increase due to frictional interactions. Typically, for a given process time where lower temperatures are used more bead impact material is required. It is possible to carry out the process at elevated temperature and, in part, this may be achieved by using heated water in the milling step. Indeed, it has been found that elevated temperature either imposed externally, for instance by use of hot water and/or thermal jacketing, or generated in-situ is associated with acceleration of the attrition process. In the case of CDs which have an acrylate outer layer overlying the metal layer, the use of elevated temperature also advantageously lowers the integrity of the acrylate layer thereby facilitating its removal.
  • the process of the mvention may therefore be carried out at elevated temperature provided that the polymeric substrate it is desired to recover is not adversely affected.
  • the polymeric substrate is a polycarbonate
  • the process may be carried out at a temperature of, for example, up to 120°C (in which case the process must be carried out under pressure). Where the process is carried out at atmospheric pressure the maximum temperature will be 100°C. In determining the temperature at which the process is carried out the temperature increase due to the milling operation itself must be accounted for.
  • Milling takes place in any suitable apparatus which is capable of causing high shear between the flakes and bead impact material.
  • a high shear mixer a stirred attrition mill, a peg mill mixer or a bead mill may be used.
  • the duration of milling will vary depending upon such factors as the shear imparted by the mixer, the type and proportion of bead impact material, the flake size and the temperature, and may be determined on a case- by-case basis for optimum results.
  • the flakes Prior to milling, it is preferred that the flakes are washed in an aqueous medium containing a detergent or surfactant suitable to remove any particulate and absorbed contaminants from the flake surface.
  • the flake is subjected to shear washing with water. Water used in this step may be recycled to the milling step in order to minimise loss of potentially valuable components.
  • the flalces of washed polymeric substrate are then separated from metal-containing material, and other materials such as derived from any overlying layer(s), using conventional techniques.
  • the separated flalces of polymeric substrate may then be dewatered and dried by conventional techniques.
  • the polymeric substrate is now in a form which may be useful for further applications. Depending upon the grade of the resulting polymer, this may include re-use in an electronic material such as a CD or DND. Alternatively, the polymeric substrate material may be used in applications where the grade ofthe material is not as critical.
  • the metal-containing material is treated to recover the metal. This may be achieved using a thickener, such as a Lamella thickener, which allows the metal solids to settle and flowover water to be removed. A conventional flocculating agent may be used in this step.
  • the metal may then be recovered by filtration techniques such as by use of a pressure filter, drum filter or belt filter. A cake of metal is obtained.
  • the scrap electronic material includes primarily polycarbonate polymers, aluminium and gold. However, a number of other materials may also be present. These include various adhesives, polymeric materials, lacquers and printing inks.
  • the polycarbonate polymer it is important and preferred that in its recovered state it is free from contaminants and also that its molecular weight has not been adversely reduced by the recovery process. Any undesirable reduction in molecular weight may be remedial increasing the molecular weight in accordance with conventional techniques. It is less important to have the gold free from other materials as the weight concentration ofthe gold is relatively low, typically only lOOppm.
  • the process may be used to recover polycarbonate and metal from a CD or DND.
  • CDs typically have a substrate layer of polycarbonate which is coated on one side with a metal backing layer (usually aluminium).
  • the CD also includes as an outer layer over the metal backing layer an acrylate layer.
  • the present invention may be applied to strip off the layer of acrylate and the layer of metal in order to isolate the polycarbonate.
  • the metal may also be recovered.
  • DNDs may be single-or double-sided. In the double-sided version a layer of metal, typically gold or a gold alloy, is sandwiched between two substrate layers of polycarbonate and acrylate layers may be provided as outer layers on the respective polycarbonate substrate layers.
  • the metal is usually bonded to the polycarbonate layers with an adhesive. In order to access the metal layer it is necessary to delaminate the DND structure. Cutting the DND into flakes usually initiates this and subsequent milling will further it.
  • the polycarbonate may be isolated as described using milling/attrition.
  • the CD or DND is cut into flakes having an even distribution of particle size of about 6mm.
  • the weight ratio of water:flake used is typically 1 : 1 and the process temperature about 80°C.
  • As bead impact material silica powder with a maximum particle size of 150 ⁇ m or polycarbonate pellets with a particle size of 1 to 2mm may be used. In either case the weight ratio ofthe bead impact material to flake is approximately 1 :20.
  • the invention may be applied to any scrap material in which a metal is provided on a polymeric substrate.
  • the invention may be used to recycle aircraft windows and vehicle headlight reflective backings.
  • the material from each of these millings was separated on the basis of size into gold rich and polymer rich fractions.
  • the polymer fraction was dewatered and dried to give a high purity compounding grade of polycarbonate.
  • 0.2kg of 6mm flakes of a CD and 0.24kg of water (heated to 80°C) were milled using a peg impeller in a 90mm diameter container surrounded by a 110mm diameter container as a water jacket.
  • the bead impact medium was lOg pumice having a maximum particle size of approximately 300 ⁇ m.
  • the impeller was operated at approximately 1500 rpm. Over the course of an hour a temperature rise of 8°C was observed (the water temperature initially fell to 72°C). After as little as a quarter of an hour the. flakes were estimated to be 99% clean.
  • Example 2 was repeated except that the container was 88mm diameter, the impeller operated at 2095rpm and the test run for 60 minutes.
  • the temperature of the water after addition to the container was recorded at 35°C rising to 65°C after a total of 60 minutes.
  • a sample taken at 30 minutes was estimated to be 97% clean.
  • a sample taken after 60 minutes was estimated to be 99%) clean.
  • Example 3 was repeated except that the pumice was replaced with lOg silica having a maximum particle size of 150 ⁇ m. After 15 minutes the water temperature was 75°C rising to 87°C after a further 15 minutes. Samples were taken at 5 and 30 minutes and were estimated to be between 95 and 97% clean.
  • Example 3 was repeated with the water temperature being 72°C after 5 minutes rising to 95°C after 15 minutes. A sample taken after 5 minutes was estimated to be 99% clean.
  • the flakes of scrap material may function as the bead impact material, i.e. it is not essential to include any extraneous abrasive in order to achieve the desired attrition.
  • the present specification may be understood with this in mind. This is particularly useful when recycling CDs.
  • the word "comprise”, and variations such as “comprises” and “comprising”, will be understood to imply the inclusion of a stated integer or step or group of integers or steps but not the exclusion of any other integer or step or group of integers or steps.

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  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
  • Processing Of Solid Wastes (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Mechanical Treatment Of Semiconductor (AREA)

Abstract

L'invention concerne un procédé de recyclage des ferrailles électroniques constituées d'un métal déposé sur un substrat polymère. Ledit procédé consiste : à broyer les ferrailles électroniques réduits en flocons au moyen d'un matériau d'impact du type billes, en présence d'eau, de manière à produire des flocons de substrat polymère nettoyé; à ajouter de l'eau aux ferrailles broyées et à séparer les flocons de substrat polymère nettoyé du matériau renfermant le métal ; à déshydrater et à sécher les flocons de substrat polymère nettoyé ; et à traiter le matériau renfermant le métal pour récupérer le métal.
PCT/AU2001/000538 2000-05-11 2001-05-11 Procede de delaminage Ceased WO2001085414A1 (fr)

Priority Applications (6)

Application Number Priority Date Filing Date Title
EP20010929117 EP1341654B1 (fr) 2000-05-11 2001-05-11 Procede de delaminage
AU5600001A AU5600001A (en) 2000-05-11 2001-05-11 Delamination process
CA002406600A CA2406600C (fr) 2000-05-11 2001-05-11 Procede de recuperation d'un substrat polymerique et de materiau metallique a partir de materiau electronique lamine
DE2001621795 DE60121795T2 (de) 2000-05-11 2001-05-11 Verfahren zur delaminierung
AU2001256000A AU2001256000B2 (en) 2000-05-11 2001-05-11 Delamination process
US10/275,679 US6793709B2 (en) 2000-05-11 2001-05-11 Delamination process

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
AUPQ7471A AUPQ747100A0 (en) 2000-05-11 2000-05-11 Delamination process
AUPQ7471 2000-05-11

Publications (1)

Publication Number Publication Date
WO2001085414A1 true WO2001085414A1 (fr) 2001-11-15

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Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/AU2001/000538 Ceased WO2001085414A1 (fr) 2000-05-11 2001-05-11 Procede de delaminage

Country Status (10)

Country Link
US (1) US6793709B2 (fr)
EP (1) EP1341654B1 (fr)
CN (1) CN100413665C (fr)
AT (1) ATE333973T1 (fr)
AU (1) AUPQ747100A0 (fr)
CA (1) CA2406600C (fr)
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004050321A1 (fr) * 2002-12-02 2004-06-17 Pirelli & C. S.P.A. Procede de pulverisation de caoutchouc vulcanise

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPWO2006070434A1 (ja) * 2004-12-27 2008-06-12 オリエント測器コンピュータ株式会社 データ記録媒体の廃棄処理方法
FR2881676B1 (fr) * 2005-02-09 2007-04-06 Cie Europ Des Matieres Plastiq Ligne de recyclage de disques optiques et de leur conditionnement

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0948025A (ja) * 1995-08-08 1997-02-18 Victor Co Of Japan Ltd 光学ディスクの基板樹脂再生方法及び再生基板樹脂材料
US6060527A (en) * 1996-04-19 2000-05-09 Teijin Chemicals Ltd Method of recovering resin

Family Cites Families (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3070553A (en) 1958-07-15 1962-12-25 Dow Chemical Co Depigmenting polymeric compositions with aldehyde settling aids
NL250016A (fr) 1959-04-18 1900-01-01
GB1221657A (en) 1967-06-29 1971-02-03 Agfa Gevaert Nv Preparation of moulding material starting from polyethylene terepthalate
US3652466A (en) 1968-07-16 1972-03-28 Du Pont Process of recovering polyester from polyester films having polymeric coatings
DE2703461C2 (de) 1977-01-28 1985-01-10 Davy McKee AG, 6000 Frankfurt Stopwerk zur Vorverdichtung zerkleinerter voluminöser Polymerabfälle
US4137393A (en) 1977-04-07 1979-01-30 Monsanto Company Polyester polymer recovery from dyed polyester fibers
DE2737693A1 (de) 1977-08-20 1979-02-22 Bayer Ag Wiedergewinnung hochwertiger polycarbonate aus polycarbonat-abfaellen
US4118346A (en) 1977-12-27 1978-10-03 The Bendix Corporation Phenolic resin recovery process
US4650126A (en) * 1984-12-26 1987-03-17 E. I. Du Pont De Nemours And Company Process for ambient temperature grinding of soft polymers
US4602046A (en) * 1985-01-22 1986-07-22 E. I. Du Pont De Nemours And Company Recovery of polyester from scrap by high shear conditions
DE3511711C2 (de) * 1985-03-29 1993-12-09 Polygram Gmbh Wiederaufbereitung hochwertiger Kunststoffe aus Abfällen und Ausschußwerkstücken
DE4039024A1 (de) 1990-09-21 1992-03-26 Bayer Ag Reinigung von polycarbonat- und polyestercarbonat-abfaellen
DE4134019A1 (de) * 1991-10-15 1993-04-22 Bayer Ag Reinigung von polycarbonat- und polyester-abfaellen
FR2693668B1 (fr) 1992-07-03 1994-10-14 Helverep Sa Procédé de valorisation de déchets d'une matière synthétique contaminés par d'autres matériaux.
US5306349A (en) 1992-11-23 1994-04-26 Sony Music Entertainment, Inc. Method for removing coatings from compact discs
EP0680501A1 (fr) 1993-01-19 1995-11-08 Unichema Chemie B.V. Composition de nettoyage
US5649785A (en) 1993-03-03 1997-07-22 Djerf; Tobin Method of treating solid waste, recovering the constituent materials for recycling and reuse, and producing useful products therefrom
US5352329A (en) 1993-12-09 1994-10-04 Xerox Corporation Removing portions of imaging member layers from a substrate
DE4344582C2 (de) * 1993-12-24 2002-08-08 Daimler Chrysler Ag Chemisch-mechanisches Entlacken von Kunststoffteilen
US5817183A (en) 1996-08-12 1998-10-06 General Electric Company Method for removing coatings from thermoplastic substrates
DE19717878A1 (de) * 1997-04-28 1998-10-29 Basf Ag Verwendung von CD-Rezyklat als Einsatzstoff für Flittereinfärbungen
US6066229A (en) 1997-07-10 2000-05-23 Sony Corporation Method of recycling disk recording medium and apparatus for recovering metal reflective film
US6060439A (en) 1997-09-29 2000-05-09 Kyzen Corporation Cleaning compositions and methods for cleaning resin and polymeric materials used in manufacture
JP3523199B2 (ja) 1998-03-16 2004-04-26 アメリカン・コモディティーズ・インコーポレーテッド 粉砕再生ポリマー粒子から有害な表面物質を除去するための方法
EP1105217A4 (fr) * 1998-05-26 2001-08-16 Mba Polymers Inc Appareil et procede permettant de favoriser la separation de differentes matieres polymeres a partir d'un melange par modification de la densite differentielle
DE19955139A1 (de) * 1999-11-17 2001-07-05 Thomas Adamec Verfahren zum Zerkleinern von Elektronikschrott
US6436197B1 (en) 2000-09-05 2002-08-20 Metss Corporation Optical media demetallization process

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0948025A (ja) * 1995-08-08 1997-02-18 Victor Co Of Japan Ltd 光学ディスクの基板樹脂再生方法及び再生基板樹脂材料
US6060527A (en) * 1996-04-19 2000-05-09 Teijin Chemicals Ltd Method of recovering resin

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
DATABASE WPI Derwent World Patents Index; Class A89, AN 1997-187672/17, XP002962416 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004050321A1 (fr) * 2002-12-02 2004-06-17 Pirelli & C. S.P.A. Procede de pulverisation de caoutchouc vulcanise
US7654477B2 (en) 2002-12-02 2010-02-02 Pirelli & C. S.P.A. Pulverization process of a vulcanized rubber material

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EP1341654A1 (fr) 2003-09-10
ES2269385T3 (es) 2007-04-01
DE60121795D1 (de) 2006-09-07
ATE333973T1 (de) 2006-08-15
US20030131688A1 (en) 2003-07-17
EP1341654A4 (fr) 2003-09-10
EP1341654B1 (fr) 2006-07-26
CN1427757A (zh) 2003-07-02
CA2406600C (fr) 2008-07-08
US6793709B2 (en) 2004-09-21
CN100413665C (zh) 2008-08-27
DE60121795T2 (de) 2007-08-23
AUPQ747100A0 (en) 2000-06-08
TW589230B (en) 2004-06-01
CA2406600A1 (fr) 2001-11-15

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